TWI737911B - Device of generating hydrogen through hydrolysis along with reduction of carbon dioxide - Google Patents

Device of generating hydrogen through hydrolysis along with reduction of carbon dioxide Download PDF

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TWI737911B
TWI737911B TW107117215A TW107117215A TWI737911B TW I737911 B TWI737911 B TW I737911B TW 107117215 A TW107117215 A TW 107117215A TW 107117215 A TW107117215 A TW 107117215A TW I737911 B TWI737911 B TW I737911B
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electrode
carbon dioxide
conversion
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oxide
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TW202003925A (en
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劉玉章
呂永方
鍾人傑
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行政院原子能委員會核能研究所
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Abstract

A device is provided to generate hydrogen through hydrolysis while carbon dioxide is reduced. The device comprises a first panel of a translucent material; a first electrode deposed at an end under the first panel; a separator membrane deposed under the first panel; a second electrode deposed under the separating membrane; and a third electrode deposed at another end under the first panel. The present invention provides an efficient device to generate hydrogen with methanation. A photocatalytic composite of reforming catalysts is developed. Therein, the composite comprises a titanium-based catalytic material and a metal-, oxide- or metal-oxide-based catalytic material. Its composition include 1~90 weight percent (wt%) of the titanium-based catalytic material and 0~10wt% pf the metal-, oxide- or metal-oxide-based catalytic material. Thus, the composite obtains very high activity and selectivity to be directly applied in both the anode and the cathode. After the catalyst electrodes are deposed under light or applied with heat or bios voltage to hydrolyze water into electrons and holes for generating hydrogen, protons (H+) are directly supplied to the cathode catalyst electrode containing carbon dioxide by passing through the separator membrane; and chemical fuels of hydrocarbons or alcohols, such as methane, methanol or the like, are obtained through reforming reduction of carbon dioxide.

Description

具水分解產氫及二氧化碳還原轉化之裝置 Device with water decomposition to produce hydrogen and carbon dioxide reduction and conversion

本發明係有關於一種可同時產氫並將二氧化碳轉化(為燃料)之裝置,尤指涉及一種可使用光照或外加偏壓直接水分解產氫及產生之氫氣可直接應用於與二氧化碳反應產生燃料,特別係指對於二氧化碳之減量提供一應用方式,且不需高溫耗能進行反應之具水分解產氫及二氧化碳還原轉化裝置。 The present invention relates to a device that can simultaneously produce hydrogen and convert carbon dioxide (to fuel), in particular to a device that can use light or an external bias to directly split water to produce hydrogen and the hydrogen produced can be directly applied to react with carbon dioxide to produce fuel , In particular, it refers to a water decomposition hydrogen production and carbon dioxide reduction conversion device that provides an application method for the reduction of carbon dioxide and does not require high temperature energy consumption for reaction.

台灣98%以上能源皆來自進口,能源自主性低,目前面臨能源轉型之中長期規劃中,政府新能源政策提出至2025年,要實現再生能源占20%、天然氣50%、及燃煤30%之發電結構,而且要能穩定供電。天然氣係世界能源結構的三大支柱之一,也是一種比較清潔具有高效能之低碳能源資源,對空氣造成之污染遠低於煤炭及石油,因此多使用天然氣以取代煤炭、石油,已成為先進國家因應二氧化碳(CO2)減量可行方案之一。天然氣之用途非常廣泛,例如發電、化工業、家用暖氣、工業鍋爐、及汽車燃料等。其中進展最大的就是發電,新技術不但降低了天然氣之發電成本,而且二氧化碳排放量最多可以比燃煤少50%。在目前的世界能源消費結構中,天然氣占24%,而我國天然氣所占比例不足5%,遠低於世界平均水準,急需提高天然氣之消費量。 Over 98% of Taiwan’s energy comes from imports, and energy autonomy is low. It is currently facing a mid- to long-term energy transition plan. The government’s new energy policy proposes to achieve 20% renewable energy, 50% natural gas, and 30% coal burning by 2025. The power generation structure must be able to provide stable power supply. Natural gas is one of the three pillars of the world's energy structure. It is also a relatively clean, high-efficiency, low-carbon energy resource. The pollution to the air is much lower than that of coal and oil. Therefore, the use of natural gas to replace coal and oil has become an advanced One of the feasible solutions for the country to reduce carbon dioxide (CO 2 ). Natural gas has a wide range of uses, such as power generation, chemical industry, household heating, industrial boilers, and automobile fuels. One of the biggest advances is power generation. The new technology not only reduces the cost of natural gas power generation, but also carbon dioxide emissions can be as much as 50% less than that of coal. In the current world energy consumption structure, natural gas accounts for 24%, while my country's natural gas accounts for less than 5%, which is far below the world average. There is an urgent need to increase natural gas consumption.

二氧化碳具有碳碳雙鍵(C=C)連結非常強,加上連接氧所以穩定性非常高,一般需要輸入非常高之外部能量來打斷其強鍵的連結鍵,因此需要外加能量來打斷其鍵結。通常反應所需之外部能量,可以加熱、電子、與照射/光子來提供;然後,這些過程分別被稱為熱化學、電化學與光化學。因此,某種形式之催化係必需的,一般來說通常必需以高壓與高溫來降低其能量屏障係不可欠缺的。 Carbon dioxide has a carbon-carbon double bond (C=C), which is very strong. Coupled with oxygen, it has very high stability. Generally, very high external energy is required to break the strong bond of the bond, so additional energy is needed to break it. Its bond. Generally, the external energy required for the reaction can be provided by heating, electrons, and irradiation/photons; then, these processes are called thermochemistry, electrochemistry, and photochemistry, respectively. Therefore, some form of catalysis is necessary. Generally speaking, high pressure and high temperature must be used to reduce the energy barrier.

以甲烷化為例就是一氧化碳與二氧化碳加氫生成甲烷,它是一個強放熱之可逆反應,反應一旦開始即迅速達到平衡。意即合成氣中一氧化碳、二氧化碳與氫氣必須在一定高溫、高壓及催化劑作用下,進行化學反應生成甲烷之過程。但是高溫(一般來說商業製程費脫法(Fischer-Tropsch)通常在800℃下反應)通常太耗能且增加成本;而且高壓下反應器設計等等都是考量因素。 Taking methanation as an example is the hydrogenation of carbon monoxide and carbon dioxide to produce methane. It is a highly exothermic and reversible reaction. Once the reaction starts, it quickly reaches equilibrium. It means that the carbon monoxide, carbon dioxide and hydrogen in the synthesis gas must undergo a chemical reaction to generate methane under a certain high temperature, high pressure and the action of a catalyst. However, high temperature (generally, the Fischer-Tropsch process in commercial processes usually reacts at 800°C) is usually too energy-consuming and increases the cost; and the design of the reactor under high pressure is a consideration.

CO2(g)+4H2(g)→CH4(g)+2H2O(g) CO 2 (g)+4H 2 (g)→CH 4 (g)+2H 2 O(g)

△H298K=-165kJ/mol △H298K=-165kJ/mol

上述反應通常在250℃與500℃之間進行。主要係藉由二氧化碳重組、二氧化碳氫化與觸媒反應而製得。由於二氧化碳為完全燃燒後之產物,熱力學性質非常穩定,因此以二氧化碳為反應原料將面臨熱力學限制之問題,但若能與其他具有較高吉布士自由能(Gibbs Free Energy)之物質一起作為反應之原料,在熱力學上較為有利,例如甲烷重組反應及氫化反應。另因二氧化碳相當穩定,常需觸媒方能在較溫和之狀態下進行化學反應,故觸媒也同時扮演相當重要之角色。 The above reaction is usually carried out between 250°C and 500°C. It is mainly produced by the recombination of carbon dioxide, hydrogenation of carbon dioxide and the reaction of catalysts. Since carbon dioxide is a product of complete combustion and its thermodynamic properties are very stable, the use of carbon dioxide as a reaction material will face the problem of thermodynamic limitations, but if it can react with other substances with higher Gibbs Free Energy (Gibbs Free Energy) The raw materials are thermodynamically more favorable, such as methane recombination reaction and hydrogenation reaction. In addition, because carbon dioxide is quite stable, catalysts are often needed to carry out chemical reactions in a relatively mild state, so catalysts also play a very important role.

相關專利包含有US8815074、US8845878、CN103974897、EP2940102、及CN105038880。其中美國US8815074專利揭示了一個以其金屬銅有機骨架結構(metal organic framework,MOF)製備二氧化碳之設備裝 置,並在不同陰極與陽極之間施加電壓以減少二氧化碳。外加電壓由-1.4V至1.2V,在0.5M碳酸氫鉀溶液中反應,其主選擇產物為甲酸。美國US8845878專利則揭示在氯化鉀(KCl)等溶液中,以各種特殊觸媒施加不同電壓由-0.5V至2V,並在PH值4~8之間產生不同之化合物及化學品。因此,二氧化碳還原轉化技術目前多為外加能量需在液體溶液進行之轉化程序,面臨產生之能耗問題,且裝置複雜穩定性須再突破。 Related patents include US8815074, US8845878, CN103974897, EP2940102, and CN105038880. Among them, the U.S. US8815074 patent discloses a device for preparing carbon dioxide with its metal organic framework (MOF). Set, and apply voltage between different cathodes and anodes to reduce carbon dioxide. The applied voltage is from -1.4V to 1.2V, and the reaction is carried out in 0.5M potassium bicarbonate solution. The main product of choice is formic acid. The US8845878 patent discloses that in potassium chloride (KCl) and other solutions, various special catalysts are used to apply different voltages from -0.5V to 2V, and produce different compounds and chemicals between pH 4-8. Therefore, carbon dioxide reduction conversion technology is currently mostly a conversion process that requires additional energy to be carried out in a liquid solution, which faces the problem of energy consumption, and the complexity and stability of the device must be broken.

二氧化碳轉化係目前世界各國積極發展之一種前瞻性科學技術,然現況上,各先進國家尚處於技術發展與測試及驗證階段,尚無商業化運轉系統問世,我國國內也還未開發出可同時分解還原轉化成燃料裝置。故,一般習用者係無法符合使用者於實際使用時之所需。 Carbon dioxide conversion is a forward-looking science and technology that is actively developed by countries all over the world. However, advanced countries are still at the stage of technological development, testing and verification, and no commercial operation system has come out, and my country has not yet developed a simultaneous decomposition system. Reduction and conversion into fuel device. Therefore, general users cannot meet the needs of users in actual use.

本發明之主要目的係在於,克服習知技藝所遭遇之上述問題並提供一種有效率之產氫與甲烷化系統,主要利用自行開發之一種光催化複合型轉化觸媒,其特徵在於由鈦系催化材料與金屬、氧化物、或金屬氧化物系催化材料複合而成,組成為鈦系催化材料1~90wt%,金屬、氧化物或金屬氧化物系催化材料至多10wt%,具有相當之高活性及選擇性,可直接置於本裝置之陰陽雙電極中,觸媒電極照光、加熱或施加偏壓後,將水溶液分解產生電子電洞分離生成氫氣(H2)後,質子(H+)經過一隔離膜直接供給給含有二氧化碳之陰極觸媒電極還原轉化成烴類或醇類化學燃料,例如甲烷或甲醇等。 The main purpose of the present invention is to overcome the above-mentioned problems encountered by the prior art and provide an efficient hydrogen production and methanation system, mainly using a self-developed photocatalytic composite conversion catalyst, which is characterized by being made of titanium Catalytic material is compounded with metal, oxide, or metal oxide-based catalytic material. The composition is titanium-based catalytic material 1~90wt%, and metal, oxide or metal oxide-based catalytic material is up to 10wt%, which has quite high activity And selectivity, it can be directly placed in the positive and negative electrodes of the device. After the catalyst electrode is illuminated, heated or biased, the aqueous solution is decomposed to produce electron holes and hydrogen gas (H 2 ) is generated. After the protons (H + ) pass An isolation membrane is directly supplied to the cathode catalyst electrode containing carbon dioxide for reduction and conversion into hydrocarbon or alcohol chemical fuels, such as methane or methanol.

本發明之次要目的係在於,提供一種以直接照光、加熱或施加偏壓還原裝置水分解及還原轉化為氫及甲烷燃料,有效達到處理二氧化碳及減量;其中,所產生之燃料可依不同之觸媒電極來做選擇,生成甲烷 或甲醇等進行使用。本裝置所產生之氫氣也可連接燃料電池進行發電,一般燃料電池具有高能量轉換效率、反應時低噪音、及低環境污染等優點;燃料電池並非一次充電電池用完即丟,也不需充電,只要持續添加氫氣燃料即可維持電力產生輸出,而且氫氣燃料之濃度越高,燃料電池之運轉壽命就越長,反應後所產生之二氧化碳也可再導入本發明所提裝置中,回收轉化使用以減低二氧化碳排放,又能增加綠色能源之生產途徑。 The secondary objective of the present invention is to provide a device that uses direct illumination, heating or bias voltage reduction device to decompose and reduce water into hydrogen and methane fuel, which can effectively treat carbon dioxide and reduce the amount; wherein, the fuel produced can be different Catalytic electrode to make a choice, generate methane Or methanol, etc. for use. The hydrogen produced by this device can also be connected to a fuel cell for power generation. Generally, fuel cells have the advantages of high energy conversion efficiency, low noise during reaction, and low environmental pollution; fuel cells are not a single rechargeable battery that is lost when it is used up, and does not need to be recharged As long as the hydrogen fuel is continuously added, the power generation output can be maintained. The higher the concentration of hydrogen fuel, the longer the operating life of the fuel cell. The carbon dioxide produced after the reaction can also be introduced into the device of the present invention for recycling and conversion. In order to reduce carbon dioxide emissions, it can increase the production of green energy.

利用光觸媒照光催化使二氧化碳還原轉換為烴類或醇類化學燃料,即利用太陽能分解水(H2O)產氫或轉化二氧化碳製備成燃料(氫氣、一氧化碳、甲醇、甲烷等),將太陽能以化學能的形式貯存起來並加以利用,將金屬觸媒還原含二氧化碳的水、或非水溶液生成烴類或醇類化學燃料、或二氧化碳通過熱化學轉化法將二氧化碳轉化為有機物加以利用。雖然目前係一種前瞻性之科學技術,但因為轉化之太陽能燃料能夠與現有的能源需求及結構應用能夠很好地匹配,因此被認為是未來太陽能轉化與利用的最佳方式之一。二氧化碳係熱力學穩定之化合物,以其為原料生產都是它的還原產物,要完成此反應需對二氧化碳進行活化,亦即需向二氧化碳輸入很高之電子形式的能量,因此開發低能耗之二氧化碳轉化及利用技術對脫碳能源系統之建立具有重要之意義。人工光合成係二氧化碳轉化及利用之創新技術,其利用太陽能激發半導體光催化材料,產生電子-電洞對,發生氧化-還原反應將二氧化碳與氫氣或水合成碳氫燃料。與其它方法相比,此反應在常溫常壓下進行,原料簡單易得,直接利用太陽能也無需耗費額外能源,可實現碳材料之循環利用,被認為是最具前景之二氧化碳轉化方法。 Use photocatalyst to reduce carbon dioxide to hydrocarbon or alcohol chemical fuel, that is, use solar energy to split water (H 2 O) to produce hydrogen or convert carbon dioxide into fuel (hydrogen, carbon monoxide, methanol, methane, etc.). It can be stored and used in the form of energy. The metal catalyst can reduce carbon dioxide-containing water or non-aqueous solution to generate hydrocarbon or alcohol chemical fuel, or carbon dioxide can be converted into organic matter by thermochemical conversion method. Although it is currently a forward-looking science and technology, it is considered to be one of the best ways to convert and utilize solar energy in the future because the converted solar fuel can match the existing energy requirements and structural applications well. Carbon dioxide is a thermodynamically stable compound. The production of carbon dioxide as a raw material is its reduction product. To complete this reaction, the carbon dioxide needs to be activated, that is, the carbon dioxide needs to be imported into the carbon dioxide in the form of high energy. Therefore, the development of low energy consumption of carbon dioxide conversion And utilization technology is of great significance to the establishment of a decarbonized energy system. Artificial photosynthesis is an innovative technology for the conversion and utilization of carbon dioxide. It uses solar energy to excite semiconductor photocatalytic materials to generate electron-hole pairs, and undergo oxidation-reduction reactions to synthesize carbon dioxide with hydrogen or water into hydrocarbon fuels. Compared with other methods, this reaction is carried out under normal temperature and pressure. The raw materials are simple and easy to obtain. The direct use of solar energy does not need to consume additional energy. It can realize the recycling of carbon materials and is considered to be the most promising carbon dioxide conversion method.

為達以上之目的,本發明係一種具水分解產氫及二氧化碳還原轉化裝置,係包括:一第一面板,為可透光材料;一第一電極,設置於該第一面板下方一端,係由1~90wt%之鈦系催化材料與至多10wt%之金屬、氧化物、或金屬氧化物系催化材料複合成一光催化複合型轉化觸媒薄膜,該第一電極與該第一面板之間距離有一間隔以形成一空間,該空間設置有一電解質層;一隔離膜,設置於該第一電極下方,係為可讓質子透過之材料;一第二電極,設置於該隔離膜下方,係由1~90wt%之鈦系催化材料與至多10wt%之金屬、氧化物、或金屬氧化物系催化材料複合成一光催化複合型轉化觸媒薄膜;以及一第三電極,設置於該第一面板下方另一端,係由1~90wt%之鈦系催化材料與至多10wt%之金屬、氧化物、或金屬氧化物系催化材料複合成一光催化複合型轉化觸媒薄膜,且該第一電極與該第三電極之間側面以一第一隔板密封固定,該第二電極與該第三電極之間加設一不完全密閉之第二隔板。 To achieve the above objectives, the present invention is a device with water splitting to produce hydrogen and carbon dioxide reduction and conversion, which includes: a first panel, which is a light-permeable material; A photocatalytic composite conversion catalyst film is composed of 1~90wt% of titanium-based catalytic material and up to 10wt% of metal, oxide, or metal oxide-based catalytic material. The distance between the first electrode and the first panel is There is a space to form a space, and the space is provided with an electrolyte layer; an isolation membrane is arranged under the first electrode and is made of a material that allows protons to pass through; a second electrode is arranged under the isolation membrane and is made of 1 ~90wt% of titanium-based catalytic material and up to 10wt% of metal, oxide, or metal oxide-based catalytic material are combined to form a photocatalytic composite conversion catalyst film; and a third electrode disposed under the first panel. One end is composed of 1~90wt% of titanium-based catalytic material and up to 10wt% of metal, oxide, or metal oxide-based catalytic material to form a photocatalytic composite conversion catalyst film, and the first electrode and the third The side surfaces between the electrodes are sealed and fixed by a first separator, and an incompletely sealed second separator is added between the second electrode and the third electrode.

於本發明上述實施例中,該第一面板係為石英、派熱克斯(pyrex)玻璃、或透明壓克力。 In the above embodiment of the present invention, the first panel is made of quartz, pyrex glass, or transparent acrylic.

於本發明上述實施例中,該第一、第二及第三電極係為鉑、鈀金、鈦、氧化鋅、或二氧化鈦。 In the foregoing embodiment of the present invention, the first, second and third electrode systems are platinum, palladium gold, titanium, zinc oxide, or titanium dioxide.

於本發明上述實施例中,該電解質層係為水溶液或含犧牲試劑之電解液。 In the above embodiments of the present invention, the electrolyte layer is an aqueous solution or an electrolyte containing a sacrificial reagent.

於本發明上述實施例中,該隔離膜係為納菲薄膜(nafion)。 In the above embodiments of the present invention, the isolation film is nafion.

於本發明上述實施例中,該第一電極及該第二電極間設置至少一偏壓導線。 In the above embodiment of the present invention, at least one bias wire is arranged between the first electrode and the second electrode.

於本發明上述實施例中,該第一電極處設置一進樣口與取樣口。 In the above-mentioned embodiment of the present invention, the first electrode is provided with a sampling port and a sampling port.

於本發明上述實施例中,該第二電極處設置一二氧化碳進樣口與燃料取樣口。 In the foregoing embodiment of the present invention, a carbon dioxide injection port and a fuel sampling port are provided at the second electrode.

1:第一電極 1: the first electrode

2:第二電極 2: second electrode

3:第三電極 3: third electrode

4:第一面板 4: The first panel

5:隔離膜 5: Isolation film

6:二氧化碳進樣口與燃料取樣口 6: Carbon dioxide injection port and fuel sampling port

7:進樣口與取樣口 7: Inlet and sampling port

8、9:偏壓導線 8, 9: Bias wire

10:第一隔板 10: The first partition

第1圖,係本發明一實施例之具水分解產氫及二氧化碳還原轉化裝置之頂視示意圖。 Figure 1 is a schematic top view of an apparatus for hydrogen production by water splitting and reduction and conversion of carbon dioxide according to an embodiment of the present invention.

第2圖,係本發明一實施例之具水分解產氫及二氧化碳還原轉化裝置之側面示意圖。 Figure 2 is a schematic side view of an embodiment of the invention with a water splitting hydrogen production and carbon dioxide reduction conversion device.

以下將參照隨附之圖式來描述本發明為達成目的所使用的技術手段與功效,而以下圖式所列舉之實施例僅為輔助說明,以利 貴審查委員瞭解,但本案之技術手段並不限於所列舉圖式。在所屬技術領域中具有通常知識者在參照說明搭配圖式下,應可輕易理解本發明之精神與原則。因此,對於所屬技術領域中具有通常知識者而言,在不脫離本發明之精神與原則下,對於本發明之各種變化及修改應為顯而易見且可輕易達成的。 The technical means and effects used by the present invention to achieve the purpose will be described below with reference to the accompanying drawings, and the embodiments listed in the following drawings are only an auxiliary explanation for your reviewers’ understanding, but the technical means in this case are not Limited to the schemes listed. Those with ordinary knowledge in the technical field should be able to easily understand the spirit and principle of the present invention by referring to the description and the accompanying drawings. Therefore, for those with ordinary knowledge in the technical field, various changes and modifications to the present invention should be obvious and easily reachable without departing from the spirit and principle of the present invention.

請參閱『第1圖及第2圖』所示,係分別為本發明一實施例之具水分解產氫及二氧化碳還原轉化裝置之頂視示意圖、及本發明一實施例之具水分解產氫及二氧化碳還原轉化裝置之側面示意圖。如圖所示:本發明係一種具水分解產氫及二氧化碳還原轉化裝置,係包括一第一面板4、一第一電極1、一隔離膜5、一第二電極2、以及一第三電極3所構成。 Please refer to "Figure 1 and Figure 2", which are the top view schematic diagrams of a water splitting hydrogen production and carbon dioxide reduction conversion device according to an embodiment of the present invention, and a water splitting hydrogen production according to an embodiment of the present invention. And the schematic side view of the carbon dioxide reduction conversion device. As shown in the figure: the present invention is a device with water decomposition to produce hydrogen and carbon dioxide reduction and conversion, which includes a first panel 4, a first electrode 1, an isolation membrane 5, a second electrode 2, and a third electrode 3 constituted.

上述所提第一面板4,其材料為可透光材料,例如石英、派熱克斯 (pyrex)玻璃、或透明壓克力。 The material of the first panel 4 mentioned above is a light-permeable material, such as quartz, Pyrex (pyrex) glass, or transparent acrylic.

該第一電極1設置於該第一面板4下方一端,係由1~90wt%之鈦系催化材料與至多10wt%之金屬、氧化物、或金屬氧化物系催化材料複合成一光催化複合型轉化觸媒薄膜,其材料例如鉑、鈀金、鈦、氧化鋅、或二氧化鈦,本實施例係為鉑/二氧化鈦;上述透光之第一面板4與該第一電極1之間距離有一間隔以形成一空間(圖中未示),該空間設置有一電解質層(圖中未示),其材料係可為水溶液或含犧牲試劑之電解液,本實施例係為硫酸水溶液。其中,該第一電極1處更設置一進樣口與取樣口7。 The first electrode 1 is arranged at the lower end of the first panel 4, and is composed of 1~90wt% of titanium-based catalytic material and up to 10wt% of metal, oxide, or metal oxide-based catalytic material to form a photocatalytic composite conversion The catalyst film is made of platinum, palladium, gold, titanium, zinc oxide, or titanium dioxide. In this embodiment, it is platinum/titanium dioxide; there is a gap between the transparent first panel 4 and the first electrode 1 to form A space (not shown in the figure), the space is provided with an electrolyte layer (not shown in the figure), and the material can be an aqueous solution or an electrolyte containing a sacrificial reagent. In this embodiment, an aqueous sulfuric acid solution is used. Wherein, the first electrode 1 is further provided with a sampling port and a sampling port 7.

該隔離膜5設置於該第一電極1與該第二電極2中間,其材料係為可讓質子(H+)透過之材料,本實施例係為納菲薄膜(nafion)。 The isolation membrane 5 is disposed between the first electrode 1 and the second electrode 2, and its material is a material that allows protons (H + ) to pass through. In this embodiment, it is a nafion film.

該第二電極2設置於該隔離膜5下方,係由1~90wt%之鈦系催化材料與至多10wt%之金屬、氧化物、或金屬氧化物系催化材料複合成一光催化複合型轉化觸媒薄膜,其材料例如鉑、鈀金、鈦、氧化鋅、或二氧化鈦,本實施例係為鉑/二氧化鈦。其中,該第二電極2處設置一二氧化碳進樣口與燃料取樣口6。 The second electrode 2 is disposed under the isolation film 5, and is composed of 1~90wt% of titanium-based catalytic material and up to 10wt% of metal, oxide, or metal oxide-based catalytic material to form a photocatalytic composite conversion catalyst The material of the thin film is platinum, palladium gold, titanium, zinc oxide, or titanium dioxide. In this embodiment, it is platinum/titanium dioxide. Wherein, the second electrode 2 is provided with a carbon dioxide injection port and a fuel sampling port 6.

該第三電極3設置於該第一面板4下方另一端,其材料與該第二電極2相同,係由1~90wt%之鈦系催化材料與至多10wt%之金屬、氧化物、或金屬氧化物系催化材料複合成一光催化複合型轉化觸媒薄膜,可提高反應轉化率,本實施例係為鉑/二氧化鈦。其中,該第一電極1與該第三電極3之間側面以一第一隔板10密封固定,該第二電極2與該第三電極3之間加設一不完全密閉之第二隔板(圖中未示),使未反應之氫與該第三電極3反應。如是,藉由上述揭露之流程構成一全新之具水分解產氫及二氧化碳還原轉化裝置。 The third electrode 3 is arranged at the other end under the first panel 4, and its material is the same as that of the second electrode 2. It is made of 1~90wt% of titanium-based catalytic material and up to 10wt% of metal, oxide, or metal oxidation The material system catalytic material is compounded into a photocatalytic composite conversion catalyst film, which can increase the reaction conversion rate. In this embodiment, platinum/titanium dioxide is used. Wherein, the side surface between the first electrode 1 and the third electrode 3 is sealed and fixed by a first separator 10, and an incompletely sealed second separator is added between the second electrode 2 and the third electrode 3. (Not shown in the figure) to make unreacted hydrogen react with the third electrode 3. If so, a brand-new hydrogen production and carbon dioxide reduction conversion device with water splitting is constructed by the above-disclosed process.

當運用時,在光照射在本發明之一種具水分解產氫及二氧化碳還原轉化裝置上時,該第一電極1便會開始吸收光能將硫酸水溶液分解轉換為電子、電洞對,質子(H+)通過隔離膜5與吸附上第二電極2上之二氧化碳(CO2)進行還原轉化反應形成烴類或醇類化學燃料,例如甲烷或甲醇等。當光照強度不足以驅動本發明之裝置時,另可於該第一電極1及該第二電極2間設置一偏壓導線8、9;或增加反應時之溫度,以驅動提升本裝置轉化成燃料之產率效果。 When used, when light is irradiated on the device with water splitting hydrogen production and carbon dioxide reduction and conversion of the present invention, the first electrode 1 will begin to absorb light energy to decompose the aqueous solution of sulfuric acid into electrons, holes, and protons ( H + ) undergoes a reduction conversion reaction with carbon dioxide (CO 2 ) adsorbed on the second electrode 2 through the isolation membrane 5 to form a hydrocarbon or alcohol chemical fuel, such as methane or methanol. When the light intensity is not enough to drive the device of the present invention, a bias wire 8, 9 can be arranged between the first electrode 1 and the second electrode 2; or the temperature during the reaction can be increased to drive the device to transform into The effect of fuel yield.

以直接照光、加熱或施加偏壓還原裝置水分解及還原轉化為氫(H2)及甲烷燃料,有效達到處理二氧化碳及減量;其中,所產生之燃料可依不同之觸媒電極來做選擇,生成甲烷或甲醇等進行使用。本裝置所產生之氫氣也可連接燃料電池進行發電,一般燃料電池具有高能量轉換效率、反應時低噪音、及低環境污染等優點;燃料電池並非一次充電電池用完即丟,也不需充電,只要持續添加氫氣燃料即可維持電力產生輸出,而且氫氣燃料之濃度越高,燃料電池之運轉壽命就越長,反應後所產生之二氧化碳也可再導入本發明所提裝置中,回收轉化使用以減低二氧化碳排放,又能增加綠色能源之生產途徑,產生可有效將二氧化碳減量,並實現碳材料之循環利用之功效。 Direct lighting, heating or bias voltage reduction device water decomposition and reduction into hydrogen (H 2 ) and methane fuel, effectively processing carbon dioxide and reducing the amount; among them, the fuel produced can be selected according to different catalyst electrodes, Generate methane or methanol for use. The hydrogen produced by this device can also be connected to a fuel cell for power generation. Generally, fuel cells have the advantages of high energy conversion efficiency, low noise during reaction, and low environmental pollution; fuel cells are not a single rechargeable battery that is lost when it is used up, and does not need to be recharged As long as the hydrogen fuel is continuously added, the power generation output can be maintained. The higher the concentration of hydrogen fuel, the longer the operating life of the fuel cell. The carbon dioxide produced after the reaction can also be introduced into the device of the present invention for recycling and conversion. In order to reduce carbon dioxide emissions, it can increase the production of green energy, which can effectively reduce the amount of carbon dioxide and realize the effect of recycling carbon materials.

[實施方式1] [Embodiment 1]

製備2.5cm x 2.5cm鉑/二氧化鈦為第一電極1、第二電極2及第三電極3,將第一電極1及第二電極2之間置入一nafion隔離膜5並固定於第1圖所示裝置之右側中;將第三電極3固定於第1圖所示裝置之左側中。透光材料的第一面板4與第一電極1之間注入覆蓋住第一電極1之硫酸水溶液為電解質層,在第二電極2下方先以氦氣(He)吹洗(purge)排除裝置中其它氣體後,再注入純二氧化碳氣體(100c.c)。 氣體溫度設定範圍從30~200℃,整個系統之操作時間從1~8小時。開啟太陽光模擬器AM1.5,由透光第一面板4照射反應,操作時間終止,經由取樣口6、7,取樣進行氣相層析(gas chromatography,GC)。經分析後與檢量線比對,氫氣可產生0.2微莫耳/小時(μmole/hr),甲烷可產生0.06μmole/hr。 Prepare 2.5cm x 2.5cm platinum/titanium dioxide as the first electrode 1, the second electrode 2 and the third electrode 3. Place a nafion isolation film 5 between the first electrode 1 and the second electrode 2 and fix it in the first figure. In the right side of the device shown; fix the third electrode 3 in the left side of the device shown in Figure 1. A sulfuric acid aqueous solution covering the first electrode 1 is injected between the first panel 4 of light-transmitting material and the first electrode 1 as an electrolyte layer. Under the second electrode 2, the purging device is purged with helium (He). After other gases, inject pure carbon dioxide gas (100c.c). The gas temperature setting range is from 30 to 200°C, and the operating time of the entire system is from 1 to 8 hours. Turn on the solar simulator AM1.5, the light-transmitting first panel 4 irradiates the reaction, the operation time is terminated, and samples are taken for gas chromatography (GC) through the sampling ports 6 and 7. After analysis and comparison with the calibration curve, hydrogen can produce 0.2 micromole/hr (μmole/hr) and methane can produce 0.06μmole/hr.

[實施方式2] [Embodiment 2]

通過外部偏壓導線8、9連接III-V電池(III-V cell)為輔助,經由透光第一面板4照射反應,溫度範圍從25~90℃,整個反應時間從1~4小時。 A III-V cell is connected via external bias wires 8 and 9 as an aid, and the light-transmitting first panel 4 irradiates the reaction, the temperature range is from 25 to 90° C., and the entire reaction time is from 1 to 4 hours.

III-V cell以AM1.5照射後電壓為2.4伏(V)、電流6.1毫安(mA)。反應後分析反應器中氣體與檢量線比對,氫氣可產生1.9μmole/hr,甲烷可產生0.44μmole/hr。 After the III-V cell is irradiated with AM1.5, the voltage is 2.4 volts (V) and the current is 6.1 milliamps (mA). After the reaction, the gas in the reactor is analyzed and compared with the calibration curve. Hydrogen can produce 1.9μmole/hr, and methane can produce 0.44μmole/hr.

由上述結果證實本發明之裝置構想包含水分解產氫技術與還原轉化技術,以此概念構想可有效產生氫氣及甲烷等燃料。未來藉由太陽能等綠能節省原有的電力能源消耗及有效減少二氧化碳的含量,有助提升能源自主性及降低溫室效應。 The above results confirm that the device concept of the present invention includes water splitting hydrogen production technology and reductive conversion technology, and this concept can effectively produce hydrogen, methane and other fuels. In the future, green energy such as solar energy will save the original electricity energy consumption and effectively reduce the carbon dioxide content, which will help improve energy independence and reduce the greenhouse effect.

藉此,本發明所提具水分解產氫及二氧化碳還原轉化裝置,可以太陽能為主進行使用搭配其它綠能來源更能提升其效率,太陽能每年滯留於地球上之能量約0.6W/m2,約等於每年1022焦耳,相當於等於全球能耗之20倍來進行利用。同時台灣之日照時數長,更須有效利用。如未來能以此太陽能為能量,可以產生低成本之氫氣作為合成甲烷之供給來源,可為台灣之能源轉型應用提供一項選擇。因為其可以實現碳回收及減量,使二氧化碳再資源化同時又能有效控制二氧化碳產生之溫室效應。本發明之目標為將二氧化碳直接分解後加氫還原,結合生 成甲烷、其它燃料或石化產品,使本裝置在二氧化碳減量、環保與高值化利用、以及化學品製造應用方面,提供了一種有效率的產氫與甲烷化系統。 As a result, the water decomposition hydrogen production and carbon dioxide reduction conversion device provided by the present invention can be used mainly with solar energy and other green energy sources to improve its efficiency. The energy of solar energy remaining on the earth every year is about 0.6W/m2, about It is equivalent to 1022 joules per year, which is equivalent to 20 times the global energy consumption for utilization. At the same time, Taiwan’s sunshine hours are long and must be used effectively. If solar energy can be used as energy in the future, low-cost hydrogen can be produced as a source of synthetic methane, which can provide an option for Taiwan’s energy transformation applications. Because it can realize carbon recovery and reduction, so that carbon dioxide can be recycled into resources while effectively controlling the greenhouse effect of carbon dioxide. The object of the present invention is to directly decompose carbon dioxide and then hydrogenate and reduce it, combined with production To methane, other fuels or petrochemical products, this device provides an efficient hydrogen production and methanation system in terms of carbon dioxide reduction, environmental protection and high-value utilization, and chemical manufacturing applications.

綜上所述,本發明係一種具水分解產氫及二氧化碳還原轉化裝置,可有效改善習用之種種缺點,能以二氧化碳做為碳源,利用化學或光化學方式將二氧化碳轉化成高價值化學品或能源產品,除可大幅降低二氧化碳回收成本及後續儲存之問題,也可因替代原需自化石燃料中獲得碳源以及較耗能之製程而降低對化石燃料之依賴度,進而使本發明之產生能更進步、更實用、更符合使用者之所須,確已符合發明專利申請之要件,爰依法提出專利申請。 In summary, the present invention is a device with water decomposition to produce hydrogen and carbon dioxide reduction and conversion, which can effectively improve the various shortcomings of conventional use. It can use carbon dioxide as a carbon source to convert carbon dioxide into high-value chemicals by chemical or photochemical methods. Or energy products, in addition to greatly reducing the cost of carbon dioxide recovery and subsequent storage problems, can also reduce the dependence on fossil fuels by replacing carbon sources originally required from fossil fuels and more energy-consuming processes, thereby making the present invention Produce that is more advanced, more practical, and more in line with the needs of users, and indeed meets the requirements of an invention patent application, and a patent application is filed in accordance with the law.

惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍;故,凡依本發明申請專利範圍及發明說明書內容所作之簡單的等效變化與修飾,皆應仍屬本發明專利涵蓋之範圍內。 However, the above are only the preferred embodiments of the present invention, and should not be used to limit the scope of implementation of the present invention; therefore, all simple equivalent changes and modifications made in accordance with the scope of the patent application of the present invention and the content of the description of the invention , Should still fall within the scope of the invention patent.

1:第一電極 1: the first electrode

2:第二電極 2: second electrode

3:第三電極 3: third electrode

4:第一面板 4: The first panel

5:隔離膜 5: Isolation film

6:二氧化碳進樣口與燃料取樣口 6: Carbon dioxide injection port and fuel sampling port

7:進樣口與取樣口 7: Inlet and sampling port

8、9:偏壓導線 8, 9: Bias wire

10:第一隔板 10: The first partition

Claims (7)

一種具水分解產氫及二氧化碳還原轉化裝置,係包括:一第一面板,為可透光材料;一第一電極,設置於該第一面板下方一端,係由1~90wt%之鈦系催化材料與至多10wt%之金屬、氧化物、或金屬氧化物系催化材料複合成一光催化複合型轉化觸媒薄膜,該第一電極與該第一面板之間距離有一間隔以形成一空間,該空間設置有一電解質層;一隔離膜,設置於該第一電極下方,係為可讓質子(H+)透過之材料;一第二電極,設置於該隔離膜下方,係由1~90wt%之鈦系催化材料與至多10wt%之金屬、氧化物、或金屬氧化物系催化材料複合成一光催化複合型轉化觸媒薄膜,其中,該第二電極處設置一二氧化碳進樣口與燃料取樣口;以及一第三電極,設置於該第一面板下方另一端,係由1~90wt%之鈦系催化材料與至多10wt%之金屬、氧化物、或金屬氧化物系催化材料複合成一光催化複合型轉化觸媒薄膜,且該第一電極與該第三電極之間側面以一第一隔板密封固定,該第二電極與該第三電極之間加設一不完全密閉之第二隔板。 A device with water decomposition to produce hydrogen and carbon dioxide reduction and conversion includes: a first panel, which is a light-permeable material; a first electrode, arranged at the lower end of the first panel, and is catalyzed by 1~90wt% titanium The material is combined with up to 10wt% of metal, oxide, or metal oxide-based catalytic material to form a photocatalytic composite conversion catalyst film. There is a distance between the first electrode and the first panel to form a space, the space An electrolyte layer is provided; an isolation membrane is arranged under the first electrode and is made of a material that allows protons (H + ) to pass through; a second electrode is arranged under the isolation membrane and is made of 1~90wt% titanium The catalytic material is combined with at most 10wt% of metal, oxide, or metal oxide-based catalytic material to form a photocatalytic composite conversion catalyst film, wherein the second electrode is provided with a carbon dioxide injection port and a fuel sampling port; and A third electrode, arranged at the other end under the first panel, is composed of 1~90wt% of titanium-based catalytic material and up to 10wt% of metal, oxide, or metal oxide-based catalytic material to form a photocatalytic composite conversion A catalyst film is used, and the side surface between the first electrode and the third electrode is sealed and fixed with a first separator, and an incompletely sealed second separator is added between the second electrode and the third electrode. 依申請專利範圍第1項所述之具水分解產氫及二氧化碳還原轉化裝置,其中,該第一面板係為石英、派熱克斯(pyrex)玻璃、或透明壓克力。 According to the first item of the scope of patent application, the device with water splitting for hydrogen production and carbon dioxide reduction and conversion, wherein the first panel is made of quartz, pyrex glass, or transparent acrylic. 依申請專利範圍第1項所述之具水分解產氫及二氧化碳還原轉化裝置,其中,該第一、第二及第三電極材料之組成係為鈦與鉑、 鈀金、氧化鋅、或二氧化鈦。 According to the first item of the scope of patent application, the device for producing hydrogen by water splitting and reducing and converting carbon dioxide, wherein the composition of the first, second and third electrode materials is titanium, platinum, Palladium, zinc oxide, or titanium dioxide. 依申請專利範圍第1項所述之具水分解產氫及二氧化碳還原轉化裝置,其中,該電解質層係為水溶液或含犧牲試劑之電解液。 According to the first item of the scope of patent application, the device with water splitting to produce hydrogen and carbon dioxide reduction and conversion, wherein the electrolyte layer is an aqueous solution or an electrolyte containing a sacrificial reagent. 依申請專利範圍第1項所述之具水分解產氫及二氧化碳還原轉化裝置,其中,該隔離膜係為納菲薄膜(nafion)。 According to the first item of the scope of patent application, the device with water splitting for hydrogen production and carbon dioxide reduction and conversion, wherein the isolation membrane is nafion. 依申請專利範圍第1項所述之具水分解產氫及二氧化碳還原轉化裝置,其中,該第一電極及該第二電極間設置至少一偏壓導線。 According to the first item of the scope of patent application, the device with water splitting to produce hydrogen and carbon dioxide reduction and conversion, wherein at least one bias wire is arranged between the first electrode and the second electrode. 依申請專利範圍第1項所述之具水分解產氫及二氧化碳還原轉化裝置,其中,該第一電極處設置一進樣口與取樣口。 According to the first item of the scope of patent application, the device with water splitting to produce hydrogen and carbon dioxide reduction and conversion, wherein the first electrode is provided with a sampling port and a sampling port.
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102812159A (en) * 2010-02-08 2012-12-05 夏普株式会社 Hydrogen Production Apparatus And Method For Producing Hydrogen
CN104164679A (en) * 2014-08-29 2014-11-26 谭延泰 Hydrogen production system through electrolysis of water, system for synthesizing methanol as well as polar plates used by two systems

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102812159A (en) * 2010-02-08 2012-12-05 夏普株式会社 Hydrogen Production Apparatus And Method For Producing Hydrogen
CN104164679A (en) * 2014-08-29 2014-11-26 谭延泰 Hydrogen production system through electrolysis of water, system for synthesizing methanol as well as polar plates used by two systems

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